### Name:

Title: Company: Sign Date: Name:
Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Wednesday, February 02, 2011 Page 1 of 32

### Facility Information:

NC_Riverbend Unit 7B

175 Steam Plant Road

Mt. Holly NC 28120
Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com Testing Company:

AECOM 2 Technology Park Drive

Westford MA 01886
Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:
03788T31 Permitted Source ID/Name: No. 2 Fuel Oil/Coal-Fired Electric Utility Boiler Unit 4-Stack 7

Permitted Maximum Process Rate:
1058 MMBtu/hr Max. Normal Operation Process Rate:
1058 MMBtu/hr Target Process Test Rate
1058 MMBtu/hr

Description of the source (including control equipment). Please see the attachments for source or process flow diagram:
This description should describe the process and associated controls to differentiate this facility from, or document similarity with others of same SCC. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 110000348641 FRS #: 3707100040

SCC / Description 10100201 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Pulverized Coal: Wet Bottom (Bituminous Coal)

The following state and federal regulations that apply to the proposed testing:

Location Round

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width

Stack Exit 102 8 2 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location

Carbon Monoxide Method 10 3 60 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 4 120 0 Stack Exit

Hydrogen Fluoride Method 26A 3 60 0 Stack Exit Hydrogen Chloride Method 26A 3 60 0 Stack Exit Organic Condensible

Particulate OTM - 27/28 3 340 0 R1-367 min, R2-346 min, R3-309min Stack Exit



### Wednesday, February 02, 2011 Page 2 of 32

### The following describes any modifications and/or deviations to the applicable test

methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates.
EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow simultaneous collection of HCl, HF and HCN. Modification included elimination of the 0.1 N H2SO4 impingers, addition of a third NaOH impinger and use of high normality NaOH absorbing solutions (6N in the 1st impinger and 2 N in the second and third) in order to maintain the pH of the solution high enough to prevent poor HCN analyte collection. The sample time was also reduced to 1-hour as allowed by EPA (see FAQ's section on the ICR website) again to ensure that the pH of the absorbing solution remained high.

Total PM2.5 OTM - 27/28 3 340 0 R1-367 min, R2-346 min, R3-309min Stack Exit

Filterable PM2.5 OTM - 27/28 3 340 0 R1-367 min, R2-346 min, R3-309min Stack Exit

Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 340 0 R1-367 min, R2-346 min, R3-309min Stack Exit

Cobalt Method 29 3 180 0 Stack Exit Manganese Method 29 3 180 0 Stack Exit Lead Method 29 3 180 0 Stack Exit Antimony Method 29 3 180 0 Stack Exit Nickel Method 29 3 180 0 Stack Exit
Arsenic Method 29 3 180 0 Stack Exit
Chromium Method 29 3 180 0 Stack Exit Selenium Method 29 3 180 0 Stack Exit Cadmium Method 29 3 180 0 Stack Exit
Filterable Particulate Method 29 3 180 0 Stack Exit Beryllium Method 29 3 180 0 Stack Exit
O2 Method 3A O2 3 60 0 Stack Exit
Co2 Method 3A CO2 3 60 0 Stack Exit Sulfur Dioxide Method 6C 3 60 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Wednesday, February 02, 2011 Page 3 of 32

### Sampling / Stack Data Results Summary



### Location Stack Exit - Method 10
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - Method 10 3
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Wednesday, February 02, 2011 Page 4 of 32

### Location Stack Exit - Method 25A
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - Method 26A
Average

Run Number CTM033- 7B-1 CTM033-

7B-2 CTM033-

7B-3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:08:00 AM 10:42:00 AM 12:25:00 PM

Run Finish Time 10:15:00 AM 11:51:00 AM 1:31:00 PM

Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 36.700 36.329 35.672 36.234
Moisture Content of Stack Gas, % 9.69 9.54 8.89 9.373 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 12.71 12.7 12.68 12.697 Oxygen, % 6.66 6.68 6.7 6.680 Average Stack Gas Temperature, °F 334.17 334.17 338.08 335.473 Dry Volumetric Flow Rate, dry scfm 121,501.0 122,322.5 124,220.7 122,681.400
Actual Wet Volumetric Flue Gas Flow Rate, acfm 207,278.1 208,333.6 211,091.4 208,901.033 Percent Isokinetic of Sampling Rate, % 106.3 104.5 101.0 103.933
F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000



### Wednesday, February 02, 2011 Page 5 of 32

### Location Stack Exit - Method 29
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Location Stack Exit - Method 3A CO2
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Wednesday, February 02, 2011 Page 6 of 32

### Location Stack Exit - Method 3A CO2 3
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - Method 3A CO2 3 6
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Wednesday, February 02, 2011 Page 7 of 32

### Location Stack Exit - Method 3A O2
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - Method 3A O2 3
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Wednesday, February 02, 2011 Page 8 of 32

### Location Stack Exit - Method 3A O2 3 6
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - Method 6C
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Wednesday, February 02, 2011 Page 9 of 32

### Location Stack Exit - Method 7E
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Stack Exit - OTM - 27/28
Average

Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Wednesday, February 02, 2011 Page 10 of 32

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average
Run CTM033-7B-1 CTM033-7B-2 CTM033-7B-3 Elb/hr 1.69E+01 1.70E+01 1.46E+01 16.167 lb/mmBtuO2 3.34E-02 3.33E-02 2.81E-02 0.032
ppm 3.20E+01 3.19E+01 2.69E+01 30.267 ppm@7%O2 3.12E+01 3.12E+01 2.63E+01 29.567



### Location: Stack Exit - Method 10 3 Compound: Carbon Monoxide Average
Run Organic-7B-1 Organic-7B-2 Organic-7B-3 Elb/hr 1.56E+01 2.12E+01 1.30E+01 16.600 lb/mmBtuO2 2.91E-02 3.99E-02 2.46E-02 0.031
ppm 2.79E+01 3.81E+01 2.37E+01 29.900 ppm@7%O2 2.72E+01 3.72E+01 2.30E+01 29.133



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average
Run 1 2 3 lb/mmBtuO2 1.64E-03 5.30E-04 9.59E-04 0.001
ppm 9.97E-01 3.22E-01 5.86E-01 0.635 ppm@7%O2 9.72E-01 3.15E-01 5.69E-01 0.619



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber CTM033-7B-1 CTM033-7B-2 CTM033-7B-3 Mass_mg 82.275 81.181 81.666 81.707 Elb/hr 3.60E+01 3.62E+01 3.76E+01 36.600 lb/mmBtuO2 7.09E-02 7.08E-02 7.27E-02 0.071 mg/dscm 7.92E+01 7.89E+01 8.09E+01 79.667 mg/dscm@7%O2 7.73E+01 7.71E+01 7.92E+01 77.867



### Compound: Hydrogen Fluoride Average RunNumber CTM033-7B-1 CTM033-7B-2 CTM033-7B-3 Mass_mg 8.86 8.43 8 8.430 Elb/hr 3.88E+00 3.75E+00 3.69E+00 3.773 lb/mmBtuO2 7.64E-03 7.35E-03 7.12E-03 0.007 mg/dscm 8.53E+00 8.20E+00 7.92E+00 8.217 mg/dscm@7%O2 8.33E+00 8.02E+00 7.75E+00 8.033



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 7B-1 7B-2 7B-3



### Wednesday, February 02, 2011 Page 11 of 32Mass_mg 0.0159 0.0012 0.00083 0.006 Elb/hr 2.00E-03 1.50E-04 1.03E-04 0.001 gr/dscf 1.85E-06 1.44E-07 9.66E-08 0.000 gr/dscf@7%O2 1.82E-06 1.41E-07 9.44E-08 0.000 lb/mmBtuO2 3.95E-06 2.98E-07 1.98E-07 0.000 mg/dscm 4.24E-03 3.30E-04 2.21E-04 0.002 mg/dscm@7%O2 4.17E-03 3.24E-04 2.16E-04 0.002 ug/dscm 4.24E+00 3.30E-01 2.21E-01 1.597 ug/dscm@7%O2 4.17E+00 3.24E-01 2.16E-01 1.570



### Compound: Arsenic Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.13705 0.09765 0.09565 0.110 Elb/hr 1.72E-02 1.22E-02 1.19E-02 0.014 gr/dscf 1.60E-05 1.17E-05 1.11E-05 0.000 gr/dscf@7%O2 1.57E-05 1.15E-05 1.09E-05 0.000 lb/mmBtuO2 3.41E-05 2.42E-05 2.29E-05 0.000 mg/dscm 3.65E-02 2.69E-02 2.55E-02 0.030 mg/dscm@7%O2 3.59E-02 2.64E-02 2.49E-02 0.029 ug/dscm 3.65E+01 2.69E+01 2.55E+01 29.633 ug/dscm@7%O2 3.59E+01 2.64E+01 2.49E+01 29.067



### Compound: Beryllium Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.0299 0.0009 0.0006 0.010 Elb/hr 3.76E-03 1.13E-04 7.45E-05 0.001 gr/dscf 3.48E-06 1.08E-07 6.99E-08 0.000 gr/dscf@7%O2 3.42E-06 1.06E-07 6.83E-08 0.000 lb/mmBtuO2 7.43E-06 2.23E-07 1.43E-07 0.000 mg/dscm 7.97E-03 2.48E-04 1.60E-04 0.003 mg/dscm@7%O2 7.83E-03 2.43E-04 1.56E-04 0.003 ug/dscm 7.97E+00 2.48E-01 1.60E-01 2.793 ug/dscm@7%O2 7.83E+00 2.43E-01 1.56E-01 2.743



### Compound: Cadmium Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.01105 0.00525 0.00009 0.005 Elb/hr 1.39E-03 6.56E-04 1.12E-05 0.001 gr/dscf 1.29E-06 6.32E-07 1.05E-08 0.000 gr/dscf@7%O2 1.27E-06 6.20E-07 1.03E-08 0.000 lb/mmBtuO2 2.75E-06 1.30E-06 2.15E-08 0.000 mg/dscm 2.95E-03 1.45E-03 2.40E-05 0.001 mg/dscm@7%O2 2.90E-03 1.42E-03 2.35E-05 0.001 ug/dscm 2.95E+00 1.45E+00 2.40E-02 1.475 ug/dscm@7%O2 2.90E+00 1.42E+00 2.35E-02 1.448



### Compound: Chromium Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.1719 0.0092 0.0094 0.064 Elb/hr 2.16E-02 1.15E-03 1.17E-03 0.008



### Wednesday, February 02, 2011 Page 12 of 32gr/dscf 2.00E-05 1.11E-06 1.09E-06 0.000 gr/dscf@7%O2 1.97E-05 1.09E-06 1.07E-06 0.000 lb/mmBtuO2 4.27E-05 2.28E-06 2.25E-06 0.000 mg/dscm 4.58E-02 2.53E-03 2.50E-03 0.017 mg/dscm@7%O2 4.50E-02 2.48E-03 2.44E-03 0.017 ug/dscm 4.58E+01 2.53E+00 2.50E+00 16.943 ug/dscm@7%O2 4.50E+01 2.48E+00 2.44E+00 16.640



### Compound: Cobalt Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.0976 0.0042 0.0032 0.035 Elb/hr 1.23E-02 5.25E-04 3.98E-04 0.004 gr/dscf 1.14E-05 5.05E-07 3.73E-07 0.000 gr/dscf@7%O2 1.12E-05 4.95E-07 3.65E-07 0.000 lb/mmBtuO2 2.43E-05 1.04E-06 7.65E-07 0.000 mg/dscm 2.60E-02 1.16E-03 8.53E-04 0.009 mg/dscm@7%O2 2.56E-02 1.14E-03 8.34E-04 0.009 ug/dscm 2.60E+01 1.16E+00 8.53E-01 9.338 ug/dscm@7%O2 2.56E+01 1.14E+00 8.34E-01 9.191



### Compound: Filterable Particulate Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 1202.6 41.9 31.9 425.467 Elb/hr 1.51E+02 5.24E+00 3.96E+00 53.400 gr/dscf 1.40E-01 5.04E-03 3.71E-03 0.050 gr/dscf@7%O2 1.38E-01 4.94E-03 3.63E-03 0.049 lb/mmBtuO2 2.99E-01 1.04E-02 7.63E-03 0.106 mg/dscm 3.21E+02 1.15E+01 8.50E+00 113.667 mg/dscm@7%O2 3.16E+02 1.13E+01 8.31E+00 111.870 ug/dscm 3.21E+05 1.15E+04 8.50E+03 113,666.667 ug/dscm@7%O2 3.16E+05 1.13E+04 8.31E+03 111,870.000



### Compound: Lead Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.14541 0.00763 0.00588 0.053 Elb/hr 1.83E-02 9.54E-04 7.30E-04 0.007 gr/dscf 1.69E-05 9.18E-07 6.85E-07 0.000 gr/dscf@7%O2 1.66E-05 9.01E-07 6.70E-07 0.000 lb/mmBtuO2 3.61E-05 1.89E-06 1.41E-06 0.000 mg/dscm 3.88E-02 2.10E-03 1.57E-03 0.014 mg/dscm@7%O2 3.81E-02 2.06E-03 1.53E-03 0.014 ug/dscm 3.88E+01 2.10E+00 1.57E+00 14.157 ug/dscm@7%O2 3.81E+01 2.06E+00 1.53E+00 13.897



### Compound: Manganese Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.1398 0.0136 0.0078 0.054 Elb/hr 1.76E-02 1.70E-03 9.69E-04 0.007 gr/dscf 1.63E-05 1.64E-06 9.08E-07 0.000 gr/dscf@7%O2 1.60E-05 1.61E-06 8.88E-07 0.000



### Wednesday, February 02, 2011 Page 13 of 32lb/mmBtuO2 3.47E-05 3.37E-06 1.86E-06 0.000 mg/dscm 3.73E-02 3.74E-03 2.08E-03 0.014 mg/dscm@7%O2 3.67E-02 3.67E-03 2.03E-03 0.014 ug/dscm 3.73E+01 3.74E+00 2.08E+00 14.373 ug/dscm@7%O2 3.67E+01 3.67E+00 2.03E+00 14.133



### Compound: Nickel Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 0.1751 0.0093 0.0069 0.064 Elb/hr 2.20E-02 1.16E-03 8.57E-04 0.008 gr/dscf 2.04E-05 1.12E-06 8.03E-07 0.000 gr/dscf@7%O2 2.01E-05 1.10E-06 7.85E-07 0.000 lb/mmBtuO2 4.35E-05 2.31E-06 1.65E-06 0.000 mg/dscm 4.67E-02 2.56E-03 1.84E-03 0.017 mg/dscm@7%O2 4.59E-02 2.51E-03 1.80E-03 0.017 ug/dscm 4.67E+01 2.56E+00 1.84E+00 17.033 ug/dscm@7%O2 4.59E+01 2.51E+00 1.80E+00 16.737



### Compound: Selenium Average
RunNumber 7B-1 7B-2 7B-3 Mass_mg 1.3769 1.3609 1.3494 1.362 Elb/hr 1.73E-01 1.70E-01 1.68E-01 0.170 gr/dscf 1.60E-04 1.64E-04 1.57E-04 0.000 gr/dscf@7%O2 1.57E-04 1.61E-04 1.53E-04 0.000 lb/mmBtuO2 3.42E-04 3.37E-04 3.23E-04 0.000 mg/dscm 3.67E-01 3.75E-01 3.60E-01 0.367 mg/dscm@7%O2 3.61E-01 3.68E-01 3.52E-01 0.360 ug/dscm 3.67E+02 3.75E+02 3.60E+02 367.333 ug/dscm@7%O2 3.61E+02 3.68E+02 3.52E+02 360.333



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average
Run CTM033-7B-1 CTM033-7B-2 CTM033-7B-3 Elb/hr 7.27E+02 7.27E+02 7.30E+02 728.000 lb/mmBtuO2 1.43E+00 1.42E+00 1.41E+00 1.420
ppm 6.00E+02 5.96E+02 5.89E+02 595.000 ppm@7%O2 5.86E+02 5.83E+02 5.77E+02 582.000



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average
Run CTM033-7B-1 CTM033-7B-2 CTM033-7B-3 Elb/hr 9.44E+01 9.82E+01 9.98E+01 97.467 lb/mmBtuO2 1.86E-01 1.92E-01 1.93E-01 0.190
ppm 1.08E+02 1.12E+02 1.12E+02 110.667 ppm@7%O2 1.05E+02 1.09E+02 1.10E+02 108.000



### Location: Stack Exit - OTM - 27/28



### Wednesday, February 02, 2011 Page 14 of 32

### Process Run Data

Compound: Filterable PM2.5 Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 540.4 18.6 18.6 192.533 Elb/hr 6.74E+01 2.55E+00 2.79E+00 24.247 gr/dscf 5.65E-02 2.10E-03 2.38E-03 0.020 gr/dscf@7%O2 5.55E-02 2.06E-03 2.33E-03 0.020 lb/mmBtuO2 1.17E-01 4.33E-03 4.90E-03 0.042



### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 7.2 18.6 28.4 18.067 Elb/hr 8.98E-01 2.55E+00 4.26E+00 2.569 gr/dscf 7.52E-04 2.10E-03 3.64E-03 0.002 gr/dscf@7%O2 7.39E-04 2.06E-03 3.56E-03 0.002 lb/mmBtuO2 1.55E-03 4.33E-03 7.47E-03 0.004



### Compound: Organic Condensible Particulate Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 465 40.5 48.3 184.600 Elb/hr 5.80E+01 5.55E+00 7.24E+00 23.597 gr/dscf 4.86E-02 4.58E-03 6.19E-03 0.020 gr/dscf@7%O2 4.78E-02 4.49E-03 6.05E-03 0.019 lb/mmBtuO2 1.00E-01 9.43E-03 1.27E-02 0.041



### Compound: Total PM2.5 Average RunNumber 7B-1 7B-2 7B-3 Mass_mg 1012.6 77.7 95.3 395.200 Elb/hr 1.26E+02 1.07E+01 1.43E+01 50.333 gr/dscf 1.06E-01 8.78E-03 1.22E-02 0.042 gr/dscf@7%O2 1.04E-01 8.61E-03 1.19E-02 0.042 lb/mmBtuO2 2.19E-01 1.81E-02 2.51E-02 0.087



### Wednesday, February 02, 2011 Page 15 of 32

### Process Run Data



### Run Name Value UOM Comments Target Value
1 Heat Input 0 Million Btus/million BTU using O2 0



### 2 Heat Input 0 Million Btus/million BTU using O2 0

3 Heat Input 0 Million Btus/million BTU using O2 0

4 Heat Input 0 Million Btus/million BTU using O2 0



### 1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0



### 4 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0



### 3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 1000 Tons/hr 0



### 2 Synfuel Firing Rate 0 1000 Tons/hr 0

3 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Synfuel Firing Rate 0 1000 Tons/hr 0



### 1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

2 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

3 Petroleum Coke Firing Rate 0 1000 Tons/hr 0



### 4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

1 Coal Gas Firing Rate 0 Ft^3/min 0

2 Coal Gas Firing Rate 0 Ft^3/min 0



### 3 Coal Gas Firing Rate 0 Ft^3/min 0

4 Coal Gas Firing Rate 0 Ft^3/min 0



### 1 Fuel Oil Firing Rate 0 gal/hr 0

2 Fuel Oil Firing Rate 0 gal/hr 0

3 Fuel Oil Firing Rate 0 gal/hr 0



### 4 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

4 Flue Gas Flow Rate 0 0



### 1 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0



### Wednesday, February 02, 2011 Page 16 of 32

### APCD Run Data

Process Lab Run Data 4 FGD Scrubber Liquor pH 0 pH 0



### 1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 4 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0



### 4 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0



### 1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0



### 4 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0



### 4 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0



### 1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 Mwe 0



### 4 Unit Gross Electrical Output 0 Mwe 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments Target Value


### 1 ELECTROSTATIC PRECIPITATOR 0 0

1 drop down lists. If not on list add description and provide detailed 0 0



### 1 desription in section 5a. 0 0

1 0 0

1 SELECTIVE NONCATALYTIC REDUCTION FOR NOX 0 0

Run Name Value UOM Comments



### Wednesday, February 02, 2011 Page 17 of 32

### Run Name Value UOM Comments



### 1 Fuel Higher Heating Value 0 Btu/lb
1 Fuel Moisture 0 %
1 Ultimate/Proximate Analysis 0
1 Fuel Chlorine Content 0 mg/kg


### 1 Fuel Fluorine Content 0 mg/kg
1 Metals Content 0 mg/kg



### Wednesday, February 02, 2011 Page 18 of 32

### Sampling / Stack Data Results Detail



### Location Stack Exit - Method 10 Average
Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 19 of 32

### Location Stack Exit - Method 10 3 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 20 of 32

### Location Stack Exit - Method 25A Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 21 of 32

### Location Stack Exit - Method 26A Average

Run Number CTM033-7B-1 CTM033- 7B-2 CTM033-7B3
Test Date 4/7/2010 4/7/2010 4/7/2010 Run Start Time 9:08:00 AM 10:42:00 AM 12:25:00 PM Run Finish Time 10:15:00 AM 11:51:00 AM 1:31:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.222 0.222 0.222 0.222 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.971 0.971 0.971 0.971 Barometric Pressure, inches of Mercury 29.28 29.28 29.28 29.280 Average Orifice Meter Differential, inches H2O 1.32 1.34 1.30 1.320 Dry Gas Meter Volume Sampled, cubic feet 39.218 39.231 38.853 39.101 Average Dry Gas Meter Temperature, °F 77.92 83.63 88.25 83.267 Dry Gas Meter Volume Sampled, dscf 36.700 36.329 35.672 36.234 Total Moisture Liquid collected, g 83.8 81.4 74 79.733 Volume of Water Vapor, standard cubic feet 3.94 3.83 3.48 3.750 Moisture Content of Stack Gas, % 9.69 9.54 8.89 9.373 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9031 0.9046 0.9111 0.906 Carbon Dioxide, % 12.71 12.7 12.68 12.697 Oxygen, % 6.66 6.68 6.7 6.680 Carbon Monoxide & Nitrogen, % 80.63 80.62 80.62 80.623 Fuel Factor 1.12 1.12 1.12 Dry Molecular Weight, lb/lb-Mole 30.30 30.30 30.30 30.300 Wet Molecular weight, lb/lb-Mole 29.11 29.13 29.21 29.150 Flue Gas Static Pressure, inches of H2O -0.91 -0.9 -0.9 -0.903 Absolute Flue Gas Pressure, inches of Mercury 29.21 29.21 29.21 29.210 Average Stack Gas Temperature, °F 334.17 334.17 338.08 335.473 Average Velocity Head, inches of H2O 0.7694832049 14925 0.777854973

618953 0.796911979

157484 0.781

Average Stack Gas Velocity, feet/second 60.88 61.19 62.00 61.357 Stack Cross-Sectional Area, square feet 56.745 56.745 56.745 56.745 Dry Volumetric Flow Rate, dry scfm 121,501.0 122,322.5 124,220.7 122,681.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 207,278.1 208,333.6 211,091.4 208,901.033 Percent Isokinetic of Sampling Rate, % 106.3 104.5 101.0 103.933 Percent Excess Air, % 45.5 45.7 45.9 45.700 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Round Duct Diameter, inches 102 102 102 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Wednesday, February 02, 2011 Page 22 of 32

### Location Stack Exit - Method 29 Average

Run Number
Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches
Fw
Fc



### Wednesday, February 02, 2011 Page 23 of 32

### Location Stack Exit - Method 3A CO2 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 24 of 32

### Location Stack Exit - Method 3A CO2 3 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 25 of 32

### Location Stack Exit - Method 3A CO2 3 6 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 26 of 32

### Location Stack Exit - Method 3A O2 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 27 of 32

### Location Stack Exit - Method 3A O2 3 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 28 of 32

### Location Stack Exit - Method 3A O2 3 6 Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 29 of 32

### Location Stack Exit - Method 6C Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 30 of 32

### Location Stack Exit - Method 7E Average

Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Wednesday, February 02, 2011 Page 31 of 32

### Location Stack Exit - OTM - 27/28 Average

Run Number
Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches
Fw
Fc



### Wednesday, February 02, 2011 Page 32 of 32